A hydrocyclone with a diameter of 250 mm is selected for a flow rate of 15...
A hydrocyclone with a diameter of 250 mm is selected for a flow rate of 15 L/s at a pressure of 140 kPa. The specific gravity of the solids is 4.8 and the volumetric concentration is 0.3. If the pressure drop between the feed and the overflow is maintained at 50 kPa, determine the corrected d50C. Assuming a discharge coefficient of 0.5 and a remaining pressure of 20 kPa at the apex, determine the underflow capacity for an apex diameter of 80 mm if the underflow density is 2000 kg/m3.
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A hydrocyclone with a diameter of 250 mm is selected for a flow
rate of 15...
2.2 A 250 mm diameter pipe is 1500 m long. When the discharge is 0.095 m3/s...
2.2 A 250 mm diameter pipe is 1500 m long. When the discharge is 0.095 m3/s in this pipe, the pressure drop between the ends of the pipe is measured as 98.06 kPa. The elevation at the end of the pipe is 10 m below its beginning. What type of flow is this? What is the equivalent sand-grain roughness of the pipe wall? What is the Hazen-Williams roughness coefficient? How much energy is dissipated by fluid friction during each hour...
A given pipe having 250 mm diameter at section A and 500 mm diameter at section...
A given pipe having 250 mm diameter at section A and 500 mm diameter at section B carries petrol of specific gravity 0.89 at the flow rate of 270 l/s. The section B is at altitude of 14 m above section A. If the pressure of the petrol at section A and section B are 190 KPa and 150 KPa respectively. 1 - Calculate the Head Loss between the two sections; 2 - Change the unit flow rate in USA...
Q 3 Ninety-eight per cent sulphuric acid is pumped at 4.5 tonne/hour through a 25 mm diameter pip...
Q 3 Ninety-eight per cent sulphuric acid is pumped at 4.5 tonne/hour through a 25 mm diameter pipe, 30 m long to a reservoir 12 m higher than the feed point. Calculate the pressure drop in the pipeline. It is given that the viscosity of acid is 25 mN.s/m2 and the density of acid is 1840 kg/m3 and the roughness of the pipe is 0.05mm. Recalculate the pressure drop if the roughness of the pipe is 0.5 mm.
Q 3...
A precision flow adjustment valve (needle valve) is used to control the flow of steam in...
A precision flow adjustment valve (needle valve) is used to control the flow of steam in a ½ inch diameter (0.0127 m) pipe that is 60 m long. The pressure drop across the pipe is 16.71 kPa when the valve is half closed. Determine the loss coefficient, KL , of the valve. The average volumetric flow rate through the pipe is 0.00206 m3/s. (Steam at 200 kPa and 300 C, 0.086*10-3 Pa*s)
(c) A venturi meter is mounted in a pipeline of diameter 150 mm, which is inclined at 30° from the horizontal. Water is flowing upwards through the pipeline. The throat diameter of the venturi meter...
(c) A venturi meter is mounted in a pipeline of diameter 150 mm, which is inclined at 30° from the horizontal. Water is flowing upwards through the pipeline. The throat diameter of the venturi meter is 90 mm. One static pressure tapping is located at the throat and another 0.3 m upstream in the pipeline. The pressure difference measured between the two tappings is 200 mm of mercury. The coefficient of discharge for the meter is 0.97. Determine the actual...
A venturi meter with a diameter of 30 cm at the entrance and 15 cm at...
A venturi meter with a diameter of 30 cm at the entrance and 15
cm at the throat, is connected to a vertical pipe of diameter 30cm
carrying oil of specific gravity 0.9. The difference in elevation
of the throat section and the entrance of the venturi meter is 30
cm. The mercury manometer shows a gauge deflection of x =
1000mm.
Determine
1) the discharge of oil; and
2) the pressure difference between the entrance section and
throat section....
(b) Water flows under gravity between two reservoirs through a pipe of length 5000m. The diameter of the pipe is 0.2 m...
(b) Water flows under gravity between two reservoirs through a pipe of length 5000m. The diameter of the pipe is 0.2 m and the roughness size is 0.04 mm. The water levels in the two reservoirs are maintained with a difference of 50 m. Determine the discharge through the pipe. Neglect all minor losses. Use the attached Moody diagram for estimation of friction factor. (10 marks) (c) In (b), now include entry loss at the upper reservoir with loss coefficient...
An orifice meter with a 2 inch diameter opening is used to measure the flow rate...
An orifice meter with a 2 inch diameter opening is used to measure the flow rate of water through a horizontal 3 inch diameter pipe. A mercury manometer is used to measure the pressure difference across the orifice. If the differential height of the manometer is 7 inches, determine the volumetric flowrate (gal/min) of water through the pipe. You may assume the discharge coefficient is 0.6.
1. A centrifugal pump performance data are shown in the following table for water. Pump speed-250...
Mechanical Lab II. Please answer asap with clear work. Thank
you!
1. A centrifugal pump performance data are shown in the following table for water. Pump speed-2500 RPM Pa or P2 (bar) P. or Pi (bar) Volume of water(L Time (sec) Input-Power (W) -0.3 20 60 100 For this data set, calculate the following i. Pump discharge capacity Q (LUs and GPM) ii. Pump head H (m and ft) iii. Fluid power Pr (Watt) iv. Brake power Pb (Watt) v....
A Venturi meter equipped with a differential pressure gage is used to measure the flow rate...
A Venturi meter equipped with a differential pressure gage is used to measure the flow rate of water at 15°C (p = 999.1 kg/m”) through a 5-cm- diameter horizontal pipe. The diameter of the Venturi neck is 3 cm, and the measured pressure drop is 5.1 kPa. Taking the discharge coefficient to be 0.98, determine the volume flow rate of water and the average velocity through the pipe. 5 cm 3 cm Differential pressure gage Is The volume flow rate...
A given pipe having 250 mm diameter at section A and 500 mm diameter at section B carries petrol of specific gravity 0.89 at the flow rate of 270 l/s. The section B is at altitude of 14 m above section A. If the pressure of the petrol at section A and section B are 190 KPa and 150 KPa respectively. 1 - Calculate the Head Loss between the two sections; 2 - Change the unit flow rate in USA...
Q 3 Ninety-eight per cent sulphuric acid is pumped at 4.5 tonne/hour through a 25 mm diameter pipe, 30 m long to a reservoir 12 m higher than the feed point. Calculate the pressure drop in the pipeline. It is given that the viscosity of acid is 25 mN.s/m2 and the density of acid is 1840 kg/m3 and the roughness of the pipe is 0.05mm. Recalculate the pressure drop if the roughness of the pipe is 0.5 mm.
Q 3...
(c) A venturi meter is mounted in a pipeline of diameter 150 mm, which is inclined at 30° from the horizontal. Water is flowing upwards through the pipeline. The throat diameter of the venturi meter is 90 mm. One static pressure tapping is located at the throat and another 0.3 m upstream in the pipeline. The pressure difference measured between the two tappings is 200 mm of mercury. The coefficient of discharge for the meter is 0.97. Determine the actual...
A venturi meter with a diameter of 30 cm at the entrance and 15
cm at the throat, is connected to a vertical pipe of diameter 30cm
carrying oil of specific gravity 0.9. The difference in elevation
of the throat section and the entrance of the venturi meter is 30
cm. The mercury manometer shows a gauge deflection of x =
1000mm.
Determine
1) the discharge of oil; and
2) the pressure difference between the entrance section and
throat section....
(b) Water flows under gravity between two reservoirs through a pipe of length 5000m. The diameter of the pipe is 0.2 m and the roughness size is 0.04 mm. The water levels in the two reservoirs are maintained with a difference of 50 m. Determine the discharge through the pipe. Neglect all minor losses. Use the attached Moody diagram for estimation of friction factor. (10 marks) (c) In (b), now include entry loss at the upper reservoir with loss coefficient...
Mechanical Lab II. Please answer asap with clear work. Thank
you!
1. A centrifugal pump performance data are shown in the following table for water. Pump speed-2500 RPM Pa or P2 (bar) P. or Pi (bar) Volume of water(L Time (sec) Input-Power (W) -0.3 20 60 100 For this data set, calculate the following i. Pump discharge capacity Q (LUs and GPM) ii. Pump head H (m and ft) iii. Fluid power Pr (Watt) iv. Brake power Pb (Watt) v....
A Venturi meter equipped with a differential pressure gage is used to measure the flow rate of water at 15°C (p = 999.1 kg/m”) through a 5-cm- diameter horizontal pipe. The diameter of the Venturi neck is 3 cm, and the measured pressure drop is 5.1 kPa. Taking the discharge coefficient to be 0.98, determine the volume flow rate of water and the average velocity through the pipe. 5 cm 3 cm Differential pressure gage Is The volume flow rate...
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